EP1673493B1 - A method of nanofibres production from a polymer solution using electrostatic spinning and a device for carrying out the method - Google Patents
A method of nanofibres production from a polymer solution using electrostatic spinning and a device for carrying out the method Download PDFInfo
- Publication number
- EP1673493B1 EP1673493B1 EP04762308A EP04762308A EP1673493B1 EP 1673493 B1 EP1673493 B1 EP 1673493B1 EP 04762308 A EP04762308 A EP 04762308A EP 04762308 A EP04762308 A EP 04762308A EP 1673493 B1 EP1673493 B1 EP 1673493B1
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- Prior art keywords
- nanofibres
- charged electrode
- electrode
- polymer solution
- air
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- 229920000642 polymer Polymers 0.000 title claims abstract description 67
- 238000000034 method Methods 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 15
- 238000010041 electrostatic spinning Methods 0.000 title claims abstract description 10
- 230000005684 electric field Effects 0.000 claims abstract description 22
- 238000009987 spinning Methods 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims description 21
- 238000003860 storage Methods 0.000 claims description 18
- 238000001035 drying Methods 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
- 239000002121 nanofiber Substances 0.000 abstract description 7
- 230000005686 electrostatic field Effects 0.000 description 7
- 239000004744 fabric Substances 0.000 description 7
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 239000002904 solvent Substances 0.000 description 5
- 239000000835 fiber Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 230000001143 conditioned effect Effects 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 238000009736 wetting Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003937 drug carrier Substances 0.000 description 1
- 238000001523 electrospinning Methods 0.000 description 1
- 238000007590 electrostatic spraying Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000007943 implant Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000000935 solvent evaporation Methods 0.000 description 1
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- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/0007—Electro-spinning
- D01D5/0061—Electro-spinning characterised by the electro-spinning apparatus
- D01D5/0076—Electro-spinning characterised by the electro-spinning apparatus characterised by the collecting device, e.g. drum, wheel, endless belt, plate or grid
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/0007—Electro-spinning
- D01D5/0061—Electro-spinning characterised by the electro-spinning apparatus
- D01D5/0069—Electro-spinning characterised by the electro-spinning apparatus characterised by the spinning section, e.g. capillary tube, protrusion or pin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y40/00—Manufacture or treatment of nanostructures
Definitions
- the invention relates to a method of nanofibres production from a polymer solution using electrostatic spinning in an electric field created by a potential difference between a rotating charged electrode and a counter electrode, in which is the polymer solution for spinning supplied into the electric field by means of the surface of a rotating charged electrode which is by a part of its surface immersed in a polymer solution, while created nanofibres are by action of electric field drift away from rotating charged electrode towards the counter electrode and then the nanofibres are stored on a device for nanofibres storage.
- the invention relates to a device for nanofibres production from a polymer solution using electrostatic spinning in an electric field created by a potential difference between a rotating charged electrode and a counter electrode, in which is the polymer solution for spinning supplied into the electric field by means of the surface of a rotating charged electrode which is by a part of its surface immersed in a polymer solution, while created nanofibres are by action of electric field drift away from rotating charged electrode towards the counter electrode and then the nanofibres are stored on a device for nanofibres storage.
- Nanofibres are used as battery separators, composite reinforcement and as pharmaceutical carriers and tissue implants carriers in medicine.
- a high specific surface of nanofibres easily accessible to gaseous and liquid media predetermines for their special sorptive properties and for their use as carriers of different active ingredients, e.g. catalysators.
- Extremely small pores in layers of nanofibres are a condition for extreme thermal insulating properties.
- Nanofibres are made of a broad range of polymers, polymer blends and from blends of polymers with low molecular additives by processes of polymer solutions forming. Unlike in on principle similar processes of polymer melts forming is in solutions processing reached smaller diameters of fibres due to lower solutions viscosities. For solutions forming is used mechanical forces of flowing gaseous medium or coulombic forces in electrostatic field. Electrostatic spinning leads to fibres of lower diameters because single forming fibres are owing to distribution of equivalent charge in their volume split in a number of filaments.
- a filter produced by electrostatic spraying is also known a filter produced by electrostatic spraying.
- the material to be sprayed is moved to the electrostatic field by a conveyor made as rotating annular electrode.
- Created nanofibers are deposited on two moving belts which are parallel to the rotating electrode. Due to continuous creation of nanofibers the concentration of polymer solution on the electrode changes and subsequently lower and lower amount of nanofibers is created. The final layer of nanofibers will be therefore non-uniform in regard to its quality and density.
- From EP 1059106 is known a device and method for producing a fine fiber structure. Liquefied polymer is curved by a system of nobles or by wetting sharp protrusion of annular rotating electrode, but both this possibilities embody above mentioned drawbacks and none of them is capable of creation of uniform planar textile composed of nanofibers.
- WO 03/016601 device for production of fibers by electrostatic spinning, by which is the polymer solution or melt brought to the planar spinning electrode by a rotating conveyor. After the polymer solution or melt reaches the edge of the plannar spinning electrode, it is spinned, and created nanofibers are deposited on collecting electrode. Disadvantages of this device rest namely in the fact, that polymer solution or melt will due to its large surface on the spinning electrode solidify and by contrast the overflowing polymer solution or melt will drop to the electric field where it could be spinned in a uncontrollable manner.
- This device is not applicable in an industrial scale because is not able of continuous electrospinning for period longer than few minutes.
- the aim of the invention is to create a method and a device industrially applicable and able to reach a high spinning capacity.
- Fig. 1 is a cross section of a device with a counter electrode surrounding a part of the circumference of a charged electrode
- Fig. 2 is a cross section of an embodiment of the device with a means for nanofibres storage outside of the space between the electrodes
- Fig. 3 is a cross section of the device, where the means for nanofibres storage is formed by a plane supporting material positioned between the electrodes in the conveyance composed of stretching elements
- Fig. 4 is an embodiment similar as Fig. 1 with a fixed electrode composed of longitudinal rods and the conveyance of plane supporting material of nanofibres arranged between these rods
- Fig. 5a to 5e is a view at various embodiments of the surface of a cylinder presenting charged electrode from the front and from the side.
- a device for nanofibres production from a polymer solution using electrostatic spinning in an electric field created by a potential difference between a charged electrode and a counter electrode consisting of a container 1 at least partly filled with a polymer solution 2 in which is by a part of its circumference immersed pivoted cylinder 3 , which is by a well-known not represented method connected to a source of DC voltage and which forms a charged electrode 30 .
- a counter electrode 40 with a different potential situated which is usually connected to earth (grounded), as described in Fig. 1 , or it is by a well-known not represented method connected to a source of DC voltage of a different polarity.
- the cylinder 3 immersed in the polymer solution 2 by the bottom part of its circumference.
- Such arrangement can be changed according to the not represented example, where with polymer solution is filled a closed container, from which is on surface of the charged electrode distributed the polymer solution or the cylinder presenting the charged electrode is in such closed container positioned, while the polymer solution is wetting for example the top part of the circumference of the cylinder, which draws on its circumference appropriate amount of the polymer solution from the container.
- the counter electrode 40 made of a perforated conducing material, e.g. sheet metal, shaped in a cylindrical surface, which forms the front end of a vacuum chamber 5 , which is connected to a vacuum source 6 .
- a part of the surface of the counter electrode 40 near the charged electrode 30 serves as a conveyance 41 for plane supporting material 72 of the nanofibres pervious to air, which is for example made of a backing fabric and which is positioned on an unreeling device 81 arranged on one side of the vacuum chamber 5 and on the reeling device 82 , which is arranged on the other side of the vacuum chamber 5 .
- the plane supporting material 72 of the nanofibres forms in itself a means 7 for nanofibres storage pervious to air.
- the polymer solution 2 container 1 is open and fitted with at least one polymer solution 2 inlet 11 and at least one polymer solution 2 outlet 12.
- the mentioned polymer solution inlet 11 and outlet 12 serves to provide circulation of the polymer solution 2 and to maintain the constant height of its level in the container 1 .
- auxiliary drying air 9 supply assigned, which can be according to the well-known manner heated up as needed, for example using a heating device arranged in the auxiliary drying air 9 supply.
- the auxiliary drying air 9 is from the space between the charged electrode 30 and the counter electrode 40 either completely or partly sucked into the vacuum chamber 5 or it comes out on the other side than it is supplied.
- the polymer solution 2 drawn by the circumference of the charged electrode 30 from the container 1 into the space between the charged electrode 30 and the counter electrode 40 , where an electric field is formed.
- the surface of the charged electrode 30 are from the polymer solution 2 formed Taylor cones of a high stability and they present places of primary formation of the nanofibres 20 .
- the formed nanofibres 20 are by the effects of electric field drift away to the counter electrode 40 and consequently they are deposited on the surface of the backing fabric presenting plane supporting material 72 of the nanofibres into a layer, which thickness is controlled using the velocity of the unreeling device 81 and the reeling device 82.
- the drift of the nanofibres 20 away of the charged electrode 30 to the counter electrode 40 is promoted by streaming of air sucked from the outer space into the vacuum chamber 5 and passing along the polymer solution 2 container 1 and the charged electrode 30 and passing through the backing fabric presenting plane supporting material 72 of the nanofibres and the counter electrode 40.
- auxiliary rods 410 forming conveyance 41 for plane supporting material 72 of the nanofibres that forms the means 7 for nanofibres storage. Nevertheless, some or all of the auxiliary rods 410 can be rotable to lower friction drag while conveying the supporting material 72 of the nanofibres.
- the conveyance for the supporting material 72 of the nanofibres can be in this embodiment composed also of rods 400 forming counter electrode 40.
- the nanofibres 20 are produced in a high number so the limiting factor of the spinning device capacity is the evaporation rate of the polymer solvent from produced nanofibres 20 and the rate of drawing off of the evaporated solvent, which would in a short period create a saturated vapour state not permitting another solvent evaporation in the space between the charged electrode 30 and the counter electrode 40.
- the device is therefore fitted with the auxiliary drying air 9 supply, which provides drawing off of the solvent vapours especially from the space between the charged electrode 30 and the counter electrode 40 . To increase the effect this auxiliary drying air 9 can be heated up.
- Fig. 2 where as well as in the embodiment according to the Fig. 1 the charged electrode 30 is pivoted and by a part of its circumference it is positioned in the polymer solution 2 , which is in the container 1 and its circulation and the level in the container 1 is maintained by flowing of the polymer solution 2 through the inlet 11 and the outlet 12 .
- the counter electrode 40 positioned composed of a system of wires or rods connected to earth (grounded) or by a well-known not represented manner connected to a source of DC voltage of opposite polarity than the charged electrode 30 .
- the nanofibres 20 directing due to the action of electric field from the charged electrode 30 to the counter electrode 40 are by the action of air stream sucked into the vacuum chamber 5 deflected from their course and are drift onto the conveyor 71 pervious to air, onto which surface they are stored in a layer, which is by the motion of the conveyor 71 carried out of the device and consequently by an appropriate not represented manner processed, conditioned or stored.
- the device fitted with the inlet 90 of auxiliary drying air 9 , which enters the device casing in the direction to the conveyor 71 pervious to air, which further promotes deflecting the nanofibres 20 from the course to the counter electrode 40 to the direction to the conveyor 71 pervious to air.
- Fig. 3 an embodiment of the device consisting of pivoted charged electrode 30 immersed by bottom part of its circumference into the polymer solution 2 .
- the counter electrode 40 composed of a system of rods parallel to the axis of rotation of the charged electrode 30 and through the space between the electrodes 30 , 40 is conveyed the plane supporting material 72 of the nanofibres using conveyance 41 composed of stretching elements 42.
- the charged electrode 30 is composed of a body able to rotate, for example a cylinder, quadrangular or multiangular prism and the like, while it is advantageous if the axis of rotation is at the same time the axis of symmetry of the used body.
- the cylinder 3 is on the circumference fitted with lugs 31 and/or recesses 32 . Examples of shapes of the cylinder surface appropriate for the charged electrode are described in the Fig. 5a to 5e , while these shapes do not limit all possible embodiments but serve only as an example. In up to now described embodiments, there is created a steady electric field between the electrodes.
- the device is possible to be fit with means for creating an intermittent electric field if it is necessary for creating or storage of the nanofibres 20 layer.
- the viscosity of the solution is 230 mPa.s at 20 °C, specific electric conductivity 31 mS/cm and surface tension 38 mN/m.
- the polymer solution 2 flows into the container 1 through an inlet 11 and flows off through an outlet 12 while the level height of the polymer solution 2 in the container 1 is maintained using the position of the outlet 12 .
- the charged electrode 30 consists of a cylinder 3 of 30 mm in diameter in the embodiment according to the Fig. 5c and it is rotating clockwise in 2,5 RPM.
- the cylinder 3 is connected to +40 kV DC voltage source.
- the device is manufactured according the Fig. 1 and throughout it is led a backing fabric forming a plane supporting material 72 of the nanofibres. Owing to the low pressure in the low pressure chamber 6 behind the counter electrode 40 pervious to air, the plane material abuts to the counter electrode 40 , which forms this way the plane material conveyance.
- the surface of the rotating cylinder 3 draws the polymer solution 2 out of the container 1 and owing to the electric field between the electrodes 30 , 40 it forms Taylor cones and the nanofibres 2 in diameters 50 to 200 nanometers.
- the nanofibres 20 are drift away to the counter electrode 40 and they are stored on the running backing fabric, where they form a layer of thickness that can be controlled by the movement speed of the backing fabric.
- an auxiliary drying air 9 of the temperature of 50°C supplied is Into the space between the electrodes.
- the layer of nanofibres is produced in the amount of 1,5 g/min for one meter length of rotating cylinder 3.
- the viscosity of the solution is 260 mPa.s at 20 °C, its specific electric conductivity has been adjusted by an addition of a small amount of aqueous NaCl solution to 25 mS/cm and the surface tension has been adjusted by addition of 0,25 % nonionogene surface active agent to 36 mN/m.
- the polymer solution 2 flows into the container 1 through an inlet 11 and flows off through an outlet 12 , where its position determines the level height of the polymer solution 2 in the container 1 .
- the cylinder 3 presenting the charged electrode is 50 mm in diameter and has a smooth surface described in the Fig. 5a .
- the cylinder 3 is connected to +40 kV DC voltage source and the wire counter electrode 40 to negative 5 kV DC voltage source.
- nanofibres 20 In the space between the charged electrode 30 and the counter electrode 40 are produced nanofibres 20 in a diameter of 50 to 200 nanometers, which are by the air sucked from the space between the electrodes 30 , 40 into the vacuum chamber 5 and using the auxiliary drying air 9 drift to the surface of the conveyor 71 pervious to air, where they are stored in a fibre layer in the amount of 1,8 g/min for one meter length of rotating cylinder.
- a method and a device according to the invention are applicable for production of layers of nanofibres in diameters from 50 to 200 nanometers. These layers can be used for filtration, as battery separators, for production of special composites, for construction of sensors with extremely low time constant, for production of protective clothes, in medicine and other fields.
Abstract
Description
- The invention relates to a method of nanofibres production from a polymer solution using electrostatic spinning in an electric field created by a potential difference between a rotating charged electrode and a counter electrode, in which is the polymer solution for spinning supplied into the electric field by means of the surface of a rotating charged electrode which is by a part of its surface immersed in a polymer solution, while created nanofibres are by action of electric field drift away from rotating charged electrode towards the counter electrode and then the nanofibres are stored on a device for nanofibres storage.
- Further the invention relates to a device for nanofibres production from a polymer solution using electrostatic spinning in an electric field created by a potential difference between a rotating charged electrode and a counter electrode, in which is the polymer solution for spinning supplied into the electric field by means of the surface of a rotating charged electrode which is by a part of its surface immersed in a polymer solution, while created nanofibres are by action of electric field drift away from rotating charged electrode towards the counter electrode and then the nanofibres are stored on a device for nanofibres storage.
- Polymer fibres with diameters between 10 nm to 1.000 nm represent a new grade of materials with some properties of extreme values. Such a typical field of use of polymer fibres layers is a filtration of gases and liquids, barrier materials for entrapment of submicron particles, bacteria and chemicals, where there is a very high filtering efficiency reached. Nanofibres are used as battery separators, composite reinforcement and as pharmaceutical carriers and tissue implants carriers in medicine. A high specific surface of nanofibres easily accessible to gaseous and liquid media predetermines for their special sorptive properties and for their use as carriers of different active ingredients, e.g. catalysators. Extremely small pores in layers of nanofibres are a condition for extreme thermal insulating properties.
- Nanofibres are made of a broad range of polymers, polymer blends and from blends of polymers with low molecular additives by processes of polymer solutions forming. Unlike in on principle similar processes of polymer melts forming is in solutions processing reached smaller diameters of fibres due to lower solutions viscosities. For solutions forming is used mechanical forces of flowing gaseous medium or coulombic forces in electrostatic field. Electrostatic spinning leads to fibres of lower diameters because single forming fibres are owing to distribution of equivalent charge in their volume split in a number of filaments.
- Up to the day known methods and devices for production of nanofibres by polymer solutions forming by an air stream are described for example in
US 6.382.526 andUS 6.520.425 . Polymer solutions are injected into a spinning jet of an annular section. The solutions are then formed by a mechanical action of an air stream delivered inside of the annulus, or as the case may be outside of this annulus, to produce fibres of diameters of 200 nm to 3.000 nm. - Forming of polymer solutions using electrostatic field of mean intensity 50.000 V/m to 500.000 elm is described in patent applications
WO 0.127.365 WO 0.250.346 US 2002/0.175.449 A1 andUS 2002/084.178 A1 . According to these solutions is the polymer solution distributed into cylindrical spinning jets withinside diameter 0,5 mm to 1,5 mm. These jets are connected to a source of DC voltage. The effluent solvent is by the electrostatic force attracted to the counter electrode, which is usually grounded and at the same time it is by this force formed into fine filaments, which are consequently split in a filament bundle of corresponding smaller diameter. Spinning is performed from one jet or an array of static or moving jets with aim to increase the capacity of the device, even coverage of counter electrode or plane supporting material moving on a surface of counter electrode or in the vicinity of its surface. - The drawback of all above mentioned methods and devices for nanofibres production is a very small amount of processed polymer material in time. In the case of nanofibres forming by mechanical forces the diameter of produced nanofibres depends among others on a ratio of air mass and polymer solution flowing through the spinning jet. While forming by coulombic force in electrostatic field, there must be formed so called Taylor cone at the throat of the spinning jet, whose existence is a requirement for fibres formation and it is conditioned by a relatively narrow range of ratio of discharge velocity of the polymer solvent from the spinning jet to the intensity of electrostatic field. The maximum adjustable intensity of electrostatic field is limited by dielectric strength of air and above this limit discharges between electrodes happen. In consequence of above mentioned circumstances and attainable concentrations of spinning polymer solutions it is possible to process approximately 0,1 g to 1 g of polymer in an hour in one spinning jet, which from the industrial point of view makes the production of nanofibres very problematic.
- From
GB 1346231 EP 1059106 is known a device and method for producing a fine fiber structure. Liquefied polymer is curved by a system of nobles or by wetting sharp protrusion of annular rotating electrode, but both this possibilities embody above mentioned drawbacks and none of them is capable of creation of uniform planar textile composed of nanofibers. - Besides is describes
WO 03/016601 - The aim of the invention is to create a method and a device industrially applicable and able to reach a high spinning capacity.
- The aim of the invention has been reached by a method according to claim 1 and by the device according to
claim 7. - Advantageous features of the method and device are in dependent claims.
- Features of preamble of
claims 1 and 7 are known fromGB 1 346 231 - Examples of a device embodiment according to the invention are schematically shown in the enclosed drawings where
Fig. 1 is a cross section of a device with a counter electrode surrounding a part of the circumference of a charged electrode,Fig. 2 is a cross section of an embodiment of the device with a means for nanofibres storage outside of the space between the electrodes,Fig. 3 is a cross section of the device, where the means for nanofibres storage is formed by a plane supporting material positioned between the electrodes in the conveyance composed of stretching elements,Fig. 4 is an embodiment similar asFig. 1 with a fixed electrode composed of longitudinal rods and the conveyance of plane supporting material of nanofibres arranged between these rods,Fig. 5a to 5e is a view at various embodiments of the surface of a cylinder presenting charged electrode from the front and from the side. - A device for nanofibres production from a polymer solution using electrostatic spinning in an electric field created by a potential difference between a charged electrode and a counter electrode consisting of a container 1 at least partly filled with a
polymer solution 2 in which is by a part of its circumference immersed pivotedcylinder 3, which is by a well-known not represented method connected to a source of DC voltage and which forms acharged electrode 30. Against a free part of the circumference of thecharged electrode 30 is acounter electrode 40 with a different potential situated, which is usually connected to earth (grounded), as described inFig. 1 , or it is by a well-known not represented method connected to a source of DC voltage of a different polarity. - In the not represented embodiments is the
cylinder 3 immersed in thepolymer solution 2 by the bottom part of its circumference. Such arrangement can be changed according to the not represented example, where with polymer solution is filled a closed container, from which is on surface of the charged electrode distributed the polymer solution or the cylinder presenting the charged electrode is in such closed container positioned, while the polymer solution is wetting for example the top part of the circumference of the cylinder, which draws on its circumference appropriate amount of the polymer solution from the container. - In the example of embodiment shown in
Fig. 1 is thecounter electrode 40 made of a perforated conducing material, e.g. sheet metal, shaped in a cylindrical surface, which forms the front end of avacuum chamber 5, which is connected to avacuum source 6. A part of the surface of thecounter electrode 40 near thecharged electrode 30 serves as aconveyance 41 forplane supporting material 72 of the nanofibres pervious to air, which is for example made of a backing fabric and which is positioned on anunreeling device 81 arranged on one side of thevacuum chamber 5 and on thereeling device 82, which is arranged on the other side of thevacuum chamber 5. In this represented embodiment theplane supporting material 72 of the nanofibres forms in itself ameans 7 for nanofibres storage pervious to air. - The
polymer solution 2 container 1 is open and fitted with at least onepolymer solution 2inlet 11 and at least onepolymer solution 2outlet 12. The mentionedpolymer solution inlet 11 andoutlet 12 serves to provide circulation of thepolymer solution 2 and to maintain the constant height of its level in the container 1. - To the space between the
charged electrode 30 and thecounter electrode 40 is anauxiliary drying air 9 supply assigned, which can be according to the well-known manner heated up as needed, for example using a heating device arranged in theauxiliary drying air 9 supply. Theauxiliary drying air 9 is from the space between thecharged electrode 30 and thecounter electrode 40 either completely or partly sucked into thevacuum chamber 5 or it comes out on the other side than it is supplied. - By rotating the
charged electrode 30, where its part of its circumference is immersed in thepolymer solution 2, is thepolymer solution 2 drawn by the circumference of thecharged electrode 30 from the container 1 into the space between thecharged electrode 30 and thecounter electrode 40, where an electric field is formed. Here on the surface of thecharged electrode 30 are from thepolymer solution 2 formed Taylor cones of a high stability and they present places of primary formation of thenanofibres 20. The formednanofibres 20 are by the effects of electric field drift away to thecounter electrode 40 and consequently they are deposited on the surface of the backing fabric presentingplane supporting material 72 of the nanofibres into a layer, which thickness is controlled using the velocity of theunreeling device 81 and thereeling device 82. - The drift of the
nanofibres 20 away of thecharged electrode 30 to thecounter electrode 40 is promoted by streaming of air sucked from the outer space into thevacuum chamber 5 and passing along thepolymer solution 2 container 1 and thecharged electrode 30 and passing through the backing fabric presentingplane supporting material 72 of the nanofibres and thecounter electrode 40. - In the embodiment shown in
Fig. 4 is thecounter electrode 40 manufactured using another appropriate method, for example fromrods 400 parallel to the pivotedcylinder 3 presenting thecharged electrode 30. Between therods 400 forming thecounter electrode 40 there are arrangedauxiliary rods 410 formingconveyance 41 forplane supporting material 72 of the nanofibres that forms themeans 7 for nanofibres storage. Nevertheless, some or all of theauxiliary rods 410 can be rotable to lower friction drag while conveying the supportingmaterial 72 of the nanofibres. The conveyance for the supportingmaterial 72 of the nanofibres can be in this embodiment composed also ofrods 400 formingcounter electrode 40. In the described device thenanofibres 20 are produced in a high number so the limiting factor of the spinning device capacity is the evaporation rate of the polymer solvent from producednanofibres 20 and the rate of drawing off of the evaporated solvent, which would in a short period create a saturated vapour state not permitting another solvent evaporation in the space between the chargedelectrode 30 and thecounter electrode 40. The device is therefore fitted with theauxiliary drying air 9 supply, which provides drawing off of the solvent vapours especially from the space between the chargedelectrode 30 and thecounter electrode 40. To increase the effect thisauxiliary drying air 9 can be heated up. - The next example according to the invention is described in
Fig. 2 , where as well as in the embodiment according to theFig. 1 the chargedelectrode 30 is pivoted and by a part of its circumference it is positioned in thepolymer solution 2, which is in the container 1 and its circulation and the level in the container 1 is maintained by flowing of thepolymer solution 2 through theinlet 11 and theoutlet 12. Against the free part of the circumference of the pivoted chargedelectrode 30, there is thecounter electrode 40 positioned composed of a system of wires or rods connected to earth (grounded) or by a well-known not represented manner connected to a source of DC voltage of opposite polarity than the chargedelectrode 30. Outside of the space between the electrodes (30, 40), where the electrostatic field is created and where by electrostatic spinning thenanofibres 20 from thepolymer solution 2 are produced, there is positioned aconveyor 71 of nanofibres pervious to air, which form thedevice 7 for nanofibres storage behind which is arranged thevacuum chamber 5 connected to thevacuum source 6. - The
nanofibres 20 directing due to the action of electric field from the chargedelectrode 30 to thecounter electrode 40 are by the action of air stream sucked into thevacuum chamber 5 deflected from their course and are drift onto theconveyor 71 pervious to air, onto which surface they are stored in a layer, which is by the motion of theconveyor 71 carried out of the device and consequently by an appropriate not represented manner processed, conditioned or stored. For the aim to increase the amount of air in the space between theelectrodes inlet 90 ofauxiliary drying air 9, which enters the device casing in the direction to theconveyor 71 pervious to air, which further promotes deflecting thenanofibres 20 from the course to thecounter electrode 40 to the direction to theconveyor 71 pervious to air. - Also in this embodiment there is a possibility of various modifications in arrangement and shape of the counter electrodes. There is also possibility to insert in front of the
conveyor 71 pervious to air a backing fabric or anotherplane supporting material 72 and the layer of thenanofibres 20 can be stored onto thisplane supporting material 72. - In the
Fig. 3 is described an embodiment of the device consisting of pivoted chargedelectrode 30 immersed by bottom part of its circumference into thepolymer solution 2. Against the free part of the circumference of the pivoted chargedelectrode 30, there is positioned thecounter electrode 40 composed of a system of rods parallel to the axis of rotation of the chargedelectrode 30 and through the space between theelectrodes plane supporting material 72 of thenanofibres using conveyance 41 composed of stretchingelements 42. - The charged
electrode 30 is composed of a body able to rotate, for example a cylinder, quadrangular or multiangular prism and the like, while it is advantageous if the axis of rotation is at the same time the axis of symmetry of the used body. Thecylinder 3 is on the circumference fitted withlugs 31 and/or recesses 32. Examples of shapes of the cylinder surface appropriate for the charged electrode are described in theFig. 5a to 5e , while these shapes do not limit all possible embodiments but serve only as an example. In up to now described embodiments, there is created a steady electric field between the electrodes. The device is possible to be fit with means for creating an intermittent electric field if it is necessary for creating or storage of thenanofibres 20 layer. - Specific examples are described below.
- The
polymer solution 2 container 1 of the device according to theFig. 1 is being filled with 12% aqueous polyvinyl alcohol solution with 88 % degree of hydrolysis of a molecular weight Mw = 85.000, containing 5 mole per cent citric acid as a crosslinking agent referred to structural units of the polymer. The viscosity of the solution is 230 mPa.s at 20 °C, specificelectric conductivity 31 mS/cm and surface tension 38 mN/m. Thepolymer solution 2 flows into the container 1 through aninlet 11 and flows off through anoutlet 12 while the level height of thepolymer solution 2 in the container 1 is maintained using the position of theoutlet 12. The chargedelectrode 30 consists of acylinder 3 of 30 mm in diameter in the embodiment according to theFig. 5c and it is rotating clockwise in 2,5 RPM. Thecylinder 3 is connected to +40 kV DC voltage source. The device is manufactured according theFig. 1 and throughout it is led a backing fabric forming aplane supporting material 72 of the nanofibres. Owing to the low pressure in thelow pressure chamber 6 behind thecounter electrode 40 pervious to air, the plane material abuts to thecounter electrode 40, which forms this way the plane material conveyance. The surface of therotating cylinder 3 draws thepolymer solution 2 out of the container 1 and owing to the electric field between theelectrodes nanofibres 2 in diameters 50 to 200 nanometers. Thenanofibres 20 are drift away to thecounter electrode 40 and they are stored on the running backing fabric, where they form a layer of thickness that can be controlled by the movement speed of the backing fabric. Into the space between the electrodes is anauxiliary drying air 9 of the temperature of 50°C supplied. The layer of nanofibres is produced in the amount of 1,5 g/min for one meter length ofrotating cylinder 3. - The
polymer solution 2 container 1 of the device according to theFig. 2 is being filled with 10% aqueous polyvinyl alcohol solution with 98 % degree of hydrolysis of a molecular weight Mw = 120.000, containing 5 mole per cent citric acid as a crosslinking agent referred to structural units of the polymer. The viscosity of the solution is 260 mPa.s at 20 °C, its specific electric conductivity has been adjusted by an addition of a small amount of aqueous NaCl solution to 25 mS/cm and the surface tension has been adjusted by addition of 0,25 % nonionogene surface active agent to 36 mN/m. Thepolymer solution 2 flows into the container 1 through aninlet 11 and flows off through anoutlet 12, where its position determines the level height of thepolymer solution 2 in the container 1. Thecylinder 3 presenting the charged electrode is 50 mm in diameter and has a smooth surface described in theFig. 5a . Thecylinder 3 is connected to +40 kV DC voltage source and thewire counter electrode 40 to negative 5 kV DC voltage source. In the space between the chargedelectrode 30 and thecounter electrode 40 are producednanofibres 20 in a diameter of 50 to 200 nanometers, which are by the air sucked from the space between theelectrodes vacuum chamber 5 and using theauxiliary drying air 9 drift to the surface of theconveyor 71 pervious to air, where they are stored in a fibre layer in the amount of 1,8 g/min for one meter length of rotating cylinder. - A method and a device according to the invention are applicable for production of layers of nanofibres in diameters from 50 to 200 nanometers. These layers can be used for filtration, as battery separators, for production of special composites, for construction of sensors with extremely low time constant, for production of protective clothes, in medicine and other fields.
Claims (16)
- A method of nanofibres production from a polymer solution (2) using electrostatic spinning in an electric field created by a potential difference between a rotating charged electrode (30) and a counter electrode (40), in which is the polymer solution (2) for spinning supplied into the electric field by means of the surface of a rotating charged electrode (30) which is by a part of its surface immersed in a polymer solution (2), while created nanofibres (20) are by action of electric field drift away from rotating charged electrode (30) towards the counter electrode (40) and then the nanofibres (20) are stored on a device (7) for nanofibres (20) storage characterized by that the nanofibres (20) are created from the surface of cylinder or quadrangular or multiangular prism charged electrode (30), while the counter electrode (40) is positioned against the free part of the circumference of the charged electrode (30) and the air between charged electrode (30) and the counter electrode (40) is sucked off.
- A method as claimed in Claim 1, characterized by that the nanofibres (20) are by the air suction off deflected from their course towards the counter electrode (40) and are led to the device (7) for nanofibres (20) storage.
- A method as claimed in any of Claims 1 or 2, characterized by that into the space between the electrodes (30, 40) is supplied an auxiliary drying air (9).
- A method as claimed in Claim 3, characterized by that at least a part of the auxiliary drying air (9) is drawn off the space in front of the device (7) for nanofibres (20) storage, without passing through this device (7).
- A method as claimed in any of Claims 3 or 4, characterized by that the auxiliary drying air (9) is heated up before entering the space between electrodes (30, 40).
- A method as claimed in any of Claims 1 to 5, characterized by that the polymer solution (2) is composed of a water solution.
- Device for nanofibres production from a polymer solution (2) using electrostatic spinning in an electric field created by a potential difference between a rotating charged electrode (30) and a counter electrode (40), in which is the polymer solution (2) for spinning supplied into the electric field by means of the surface of a rotating charged electrode (30) which is by a part of its surface immersed in a polymer solution (2), while created nanofibres (20) are by action of electric field drift away from rotating charged electrode (30) towards the counter electrode (40) and then the nanofibres (20) are stored on a device (7) for nanofibres (20) storage characterized by that the charged electrode (30) is a cylinder or quadrangular or multiangular prism and against the free part of the circumference of the charged electrode (30), there is the counter electrode (40) positioned.
- Device as claimed in Claim 7, characterized by that the counter electrode (40) surrounds the free parts of the circumference of the charged electrode (30) along its entire length.
- A device as claimed in Claim 7 or 8, characterized by that between both electrodes (30, 40) is situated the device (7) for nanofibres storage.
- A device as claimed in Claim 9, characterized by that the device (7) for nanofibres storage is pervious to air, while the space behind this device (7) in regard to the charged electrode (30) is connected to the vacuum source (6).
- A device as claimed in Claim 7, characterized by that outside of the space between the electrodes (30, 40) there is positioned the device (7) for nanofibres storage pervious to air, while the space behind this device (7) in regard to the charged electrode (30) is connected to the vacuum source (6) serving to create an air stream directing towards this device (7).
- A device as claimed in any of Claims 7 to 11, characterized by that the device (7) for nanofibres storage is composed of a conveyor (71) pervious to air.
- A device as claimed in any of Claims 7 to 11, characterized by that the device (7) for nanofibres storage is composed of a plane supporting material of the nanofibres (72).
- A device as claimed in any of Claims 7 to 13, characterized by that into the space between the electrodes (30, 40) leads an inlet (90) of auxiliary drying air (9).
- A device as claimed in Claim 14, characterized by that in the inlet (90) of auxiliary drying air (9), there is positioned an air heating device.
- A device as claimed in Claim 13 or 15, characterized by that at least a part of air is drawn off the space in front of the device (7) for nanofibres storage in regard of the charged electrode (30), without passing through this device (7).
Priority Applications (3)
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SI200431232T SI1673493T1 (en) | 2003-09-08 | 2004-09-08 | A method of nanofibres production from a polymer solution using electrostatic spinning and a device for carrying out the method |
PL04762308T PL1673493T3 (en) | 2003-09-08 | 2004-09-08 | A method of nanofibres production from a polymer solution using electrostatic spinning and a device for carrying out the method |
CY20091101034T CY1110534T1 (en) | 2003-09-08 | 2009-10-07 | METHOD OF MANUFACTURING NANOINS FROM POLYMER SOLUTION USING ELECTROSTATIC SOLUTION AND APPLIANCE FOR IMPLEMENTING THE METHOD |
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CZ20032421A CZ294274B6 (en) | 2003-09-08 | 2003-09-08 | Process for producing nanofibers from polymeric solution by electrostatic spinning and apparatus for making the same |
PCT/CZ2004/000056 WO2005024101A1 (en) | 2003-09-08 | 2004-09-08 | A method of nanofibres production from a polymer solution using electrostatic spinning and a device for carrying out the method |
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DK1673493T3 (en) | 2009-11-16 |
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JP2007505224A (en) | 2007-03-08 |
ZA200601791B (en) | 2006-10-25 |
CY1110534T1 (en) | 2015-04-29 |
DE602004021951D1 (en) | 2009-08-20 |
US20060290031A1 (en) | 2006-12-28 |
KR20060079211A (en) | 2006-07-05 |
RU2006108868A (en) | 2006-08-10 |
CA2536595C (en) | 2011-08-02 |
EP1673493A1 (en) | 2006-06-28 |
AU2004270787A1 (en) | 2005-03-17 |
ATE435934T1 (en) | 2009-07-15 |
KR101143934B1 (en) | 2012-05-09 |
CN1849418B (en) | 2012-07-04 |
IL173881A0 (en) | 2006-07-05 |
SI1673493T1 (en) | 2009-12-31 |
JP4439012B2 (en) | 2010-03-24 |
CZ294274B6 (en) | 2004-11-10 |
WO2005024101A1 (en) | 2005-03-17 |
PL1673493T3 (en) | 2009-12-31 |
US7585437B2 (en) | 2009-09-08 |
AU2004270787B2 (en) | 2010-06-17 |
IL173881A (en) | 2010-11-30 |
CN1849418A (en) | 2006-10-18 |
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